JP2000110201A - Water intake device - Google Patents
Water intake deviceInfo
- Publication number
- JP2000110201A JP2000110201A JP10285402A JP28540298A JP2000110201A JP 2000110201 A JP2000110201 A JP 2000110201A JP 10285402 A JP10285402 A JP 10285402A JP 28540298 A JP28540298 A JP 28540298A JP 2000110201 A JP2000110201 A JP 2000110201A
- Authority
- JP
- Japan
- Prior art keywords
- air
- intake
- water
- atmosphere
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Drying Of Gases (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は取水装置に関し、詳
しくは、大気温度が低い場合であっても大気中の湿分か
ら水を効率よく取り出す装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water intake apparatus, and more particularly, to an apparatus for efficiently extracting water from atmospheric moisture even when the atmospheric temperature is low.
【０００２】[0002]
【従来の技術】これまで種々の取水装置が開発されてき
たが、例えば、海水淡水化といった目的には、古くから
ある蒸留法に代わって、効率の高い、逆浸透膜を利用し
た装置や限外濾過法を利用した装置などが開発された。
なかでも、エネルギー的に有利な面が多いことから逆浸
透膜を利用した装置が考えられた。しかし、逆浸透膜を
利用した装置では、膜自体が高価であり、膜の寿命がそ
れほど長くないことと相まって装置全体のコストが高い
という問題があった。しかも、膜の劣化を直接的に感知
する方法がなく、生成される淡水の水質を常時検査する
必要があり、維持コストも高いものであった。そこで、
本発明者は高価な逆浸透膜を利用することなく、安価で
簡易に真水を製造することの可能な装置を開発した。2. Description of the Related Art Various water intake devices have been developed so far. For example, for the purpose of seawater desalination, a high-efficiency device using a reverse osmosis membrane instead of a long-standing distillation method or a limited one is used. Devices utilizing the external filtration method have been developed.
Among them, an apparatus using a reverse osmosis membrane has been considered because of its many advantages in terms of energy. However, in a device using a reverse osmosis membrane, there is a problem that the cost of the whole device is high in combination with the fact that the membrane itself is expensive and the life of the membrane is not so long. In addition, there is no method for directly sensing the deterioration of the membrane, and it is necessary to constantly check the quality of the generated fresh water, and the maintenance cost is high. Therefore,
The present inventor has developed an apparatus capable of easily producing fresh water at low cost without using an expensive reverse osmosis membrane.
【０００３】[0003]
【発明が解決しようとする課題】しかしながら、上記装
置は大気が低温の場合、取水効率が低下するという問題
があった。つまり、大気温度は低いほど取水効率は低下
し、特に、大気温度が５℃を下回る場合、著しく取水効
率は低下して、使用に制限が生じるに至った。そこで本
発明者は、冬季のように大気温度が低い場合にも取水効
率を一定以上に維持させるため鋭意研究・努力した結
果、簡単な装置を加えることにより予想外の効果を発揮
し得、大気が低温である冬季においても、大気中より効
率よく取水可能な装置を発明した。However, the above-mentioned apparatus has a problem that when the atmosphere is at a low temperature, the water intake efficiency is reduced. In other words, the lower the atmospheric temperature, the lower the water intake efficiency. In particular, when the air temperature is lower than 5 ° C., the water intake efficiency is remarkably reduced, and the use is restricted. Therefore, the present inventor has conducted intensive research and efforts to maintain the intake efficiency at or above a certain level even when the atmospheric temperature is low as in winter, and as a result, unexpected effects can be exhibited by adding a simple device, Invented a device that can take water more efficiently than in the air even in winter when the temperature is low.
【０００４】本発明は、大気が低温にも関わらず効率よ
く大気中から水分を取り入れることが可能な取水装置を
提供することを目的とする。[0004] It is an object of the present invention to provide a water intake device capable of efficiently taking in moisture from the atmosphere even when the atmosphere is at a low temperature.
【０００５】[0005]
【課題を解決するための手段】上記目的は請求項記載の
発明により達成される。すなわち、本発明に係る取水措
置の特徴構成は、大気取入装置と、取り入れた大気を昇
温可能な加温装置と、前記大気取入装置によって取り入
れられる大気圧力を低減する機構を備えると共に取り入
れられた大気を冷却して湿分を取出す冷却部を内蔵した
大気湿度変換機と、この大気湿度変換機によって得られ
る水を取出す取水口とを有することにある。このように
構成されていると、冬季のように例え大気が低温にも関
わらず、大気中の湿分を増大させることができ、しか
も、採り入れる大気の温度を高くできるため、大気圧力
を小さくする必要がない。従って、採り入れる大気量を
大きくできて大量の大気の中に存在する湿分から取水が
可能となるという予期せぬ効果を発揮し得、大気環境温
度が高い場合よりもかえって取水効率が高まり、その結
果、大気が低温にも関わらず効率よく大気中から水分を
取り入れることが可能な取水装置を提供することができ
た。The above object is achieved by the invention described in the claims. That is, the characteristic structure of the water intake measure according to the present invention includes an air intake device, a heating device capable of raising the temperature of the intake air, and a mechanism for reducing the atmospheric pressure introduced by the air intake device. The present invention has an atmospheric humidity converter incorporating a cooling unit for cooling the obtained atmosphere to extract moisture, and a water intake for extracting water obtained by the atmospheric humidity converter. With such a configuration, even if the atmosphere is low in temperature as in winter, the moisture in the atmosphere can be increased, and the temperature of the introduced air can be increased, so that the atmospheric pressure is reduced. No need. Therefore, it is possible to obtain an unexpected effect that it is possible to increase the amount of air to be taken and to take water from the moisture present in a large amount of air, and the water intake efficiency is improved rather than when the atmospheric environmental temperature is high. In addition, a water intake device capable of efficiently taking in moisture from the atmosphere despite the low temperature of the atmosphere could be provided.
【０００６】前記大気取入装置によって取り入れた大気
を流量調節するための風量調節装置を備えることが好ま
しい。このようになっていると、大気取入装置に接続さ
れる大気湿度変換機が多数である場合にも、各大気湿度
変換機に送給される大気風量が均一に分岐・送給され
て、各大気湿度変換機での取水効率を平均的に高いもの
に維持できて都合がよい。[0006] It is preferable to provide an air volume adjusting device for adjusting the flow rate of the air taken in by the air intake device. With this configuration, even when there are a large number of atmospheric humidity converters connected to the atmospheric intake device, the amount of atmospheric air sent to each atmospheric humidity converter is uniformly branched and sent, It is convenient that the water intake efficiency of each atmospheric humidity converter can be maintained on average high.
【０００７】前記風量調節装置の後送風量と前記加温装
置の加温条件とを制御可能な制御装置を備えることが好
ましい。このようになっていると、風量調節装置から後
送される風量を適正なものとすると共に、加温装置の加
温条件を適正なものとできるので、常時取水効率を高く
維持できる。特に、風量調節装置から複数の分岐管など
を介して後送される場合に、各分岐管内の風量を均一に
なって取水効率の向上に寄与できるものとなる。[0007] It is preferable that the apparatus further comprises a control device capable of controlling the amount of air sent after the air volume adjusting device and the heating conditions of the heating device. With such a configuration, the air volume sent from the air volume adjusting device can be made appropriate and the heating conditions of the heating device can be made appropriate, so that the water intake efficiency can be constantly maintained at a high level. In particular, when the air is sent from the air flow adjusting device via a plurality of branch pipes or the like, the air flow in each branch pipe becomes uniform, which can contribute to an improvement in water intake efficiency.
【０００８】前記大気圧力低減機構が、大気取入口に設
けられた５０〜１２０メッシュの多孔質通気体であるこ
とが好ましい。このようになっていると、低コストで効
果的に目的を達成できて一層好ましい。この場合、大気
中の塵芥を除くこともできるので、より清浄な水が得ら
れると共に、装置自体の耐久性も向上する。通気体の孔
サイズが５０メッシュ未満では、大気圧力が大きくな
り、残留する湿分は少なくなり、得られる湿分も少なく
なって効率的でなくなるので好ましくない。通気体の孔
サイズが１２０メッシュを越えると、残留する湿分は多
くなり、得られる湿分も多くなるが、取入れる大気量を
多くすることができず、効率が低下して好ましくない。
通気体の材質としては、発泡ポリウレタン製、発泡ポリ
プロピレン製などを使用することが耐久性においても、
コスト的にも好ましい。尚、大気圧力は１６ｋｇｆ／ｃ
ｍ2 以下、より好ましくは９ｋｇｆ／ｃｍ2 以下に低減
することが取水効率を高める上で好ましい。[0008] It is preferable that the atmospheric pressure reducing mechanism is a 50-120 mesh porous vent provided at an atmospheric intake. This is more preferable because the object can be effectively achieved at low cost. In this case, dust in the atmosphere can be removed, so that cleaner water can be obtained and the durability of the device itself can be improved. If the pore size of the ventilation body is less than 50 mesh, the atmospheric pressure increases, the remaining moisture decreases, and the obtained moisture decreases, which is not preferable because it is not efficient. If the pore size of the ventilation body exceeds 120 mesh, the remaining moisture increases and the obtained moisture also increases, but the amount of air to be taken in cannot be increased, and the efficiency decreases, which is not preferable.
As for the material of the ventilation body, it is possible to use foamed polyurethane, foamed polypropylene, etc.
It is also preferable in terms of cost. Atmospheric pressure is 16kgf / c
m 2 or less, more preferably 9 kgf / cm 2 or less, from the viewpoint of increasing water intake efficiency.
【０００９】前記大気湿度変換機と取水口との間に殺菌
装置を備えることが好ましい。このようになっている
と、得られた水を飲料水に使用できるのみならず、精密
部品の洗浄水等とくに清浄な水が要求される用途に使用
できる。It is preferable that a sterilizer is provided between the atmospheric humidity converter and the water intake. In this case, the obtained water can be used not only for drinking water but also for applications requiring particularly clean water, such as cleaning water for precision parts.
【００１０】[0010]
【発明の実施の形態】本発明にかかる取水装置の一実施
形態を、図面を参照して詳細に説明する。図１は、飲料
水を得るための取水装置の全体構造を示す。この装置
は、取り入れた大気中の湿分を取出すための大気湿度変
換機１と、この大気湿度変換機１に大量の大気を取り入
れるための大気取入装置たる吸引ポンプ２と、大気湿度
変換機１に取り入れられた大気を冷却する冷媒を送込む
冷却機構３とを備える。吸引ポンプ２には、取り入れる
大気を昇温するための加温装置２ａが設けられている。
この加温装置２ａは、電熱線などからなるヒータを内蔵
していて、温度センサー（図示略）で大気の加温状態を
モニターしながら、大気が一定温度以上になるように制
御されている。この場合の温度制御は、制御装置Ｃによ
ってなされる。加温は、例えば、冬などの寒冷期に大気
が０℃近い場合に、大気を２０〜５０℃、より好ましく
は４０〜５０℃に加熱することにより、大気中の飽和水
分量を高めて、季節に関わらず効率よく大気中から取水
を可能とするものである。従って、この加温装置を備え
ることにより、本実施形態の取水装置を寒冷地方でも効
率的に使用することができる。しかも、取り入れられる
大気が加温されているので、後述する大気圧力低減機構
による大気圧力低減量を少なくして、多量の大気を取り
入れることができ、従来の装置に比べて取水効率が極め
て高いものに実現できた。尚、前記加温装置としては赤
外線輻射ヒータのような構成のものでもよい。DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of a water intake device according to the present invention will be described in detail with reference to the drawings. FIG. 1 shows the entire structure of a water intake device for obtaining drinking water. This apparatus includes an atmospheric humidity converter 1 for extracting the moisture in the air taken in, a suction pump 2 as an air intake device for introducing a large amount of air into the atmospheric humidity converter 1, and an air humidity converter. And a cooling mechanism 3 for sending a refrigerant for cooling the air taken into the cooling device 1. The suction pump 2 is provided with a heating device 2a for raising the temperature of the intake air.
The heating device 2a has a built-in heater composed of a heating wire or the like, and is controlled so that the temperature of the atmosphere becomes equal to or higher than a predetermined temperature while monitoring the heating state of the atmosphere with a temperature sensor (not shown). The temperature control in this case is performed by the control device C. Heating is, for example, when the atmosphere is close to 0 ° C in a cold season such as winter, by heating the atmosphere to 20 to 50 ° C, more preferably 40 to 50 ° C, thereby increasing the amount of saturated moisture in the atmosphere, It enables efficient water intake from the atmosphere regardless of the season. Therefore, by providing this heating device, the water intake device of the present embodiment can be used efficiently even in cold regions. Moreover, since the intake air is heated, a large amount of air can be taken in by reducing the amount of atmospheric pressure reduction by the atmospheric pressure reduction mechanism described later, and the water intake efficiency is extremely higher than that of the conventional device. Was realized. The heating device may have a configuration such as an infrared radiation heater.
【００１１】吸引ポンプ２により吸引された大量の大気
を一時に送給することによる弊害を緩和するため、吸引
した大気を２〜４に分岐する風量調節機３に送給し、こ
こで複数の大気流として分岐され、幾分整流されて変動
幅の少ない大気が次のフィルター４に送給される。つま
り、風量調節機３の内部には、図示はしないが、風量を
調節可能に開閉するダンパーが装着されていて、前記制
御装置Ｃの指示により次のフィルター４に送給される各
分岐管内の風量を均一になるように、ダンパーの開閉量
を制御するようになっている。もっとも、風量調節機３
は必ずしも必要ではないが、安定して大量の大気を送給
し、取水効率を上げるためには、設けることが好まし
い。風量調節機３によって分岐される数、分岐管のサイ
ズ等は適宜選択することができる。In order to mitigate the adverse effects caused by sending a large amount of air sucked by the suction pump 2 at one time, the sucked air is sent to an air volume controller 3 branching into two to four, where a plurality of air are sent. The air which is branched as an air flow, is somewhat rectified, and has a small fluctuation range is supplied to the next filter 4. In other words, although not shown, a damper that opens and closes so as to adjust the air flow is mounted inside the air flow adjuster 3, and the inside of each branch pipe fed to the next filter 4 according to the instruction of the control device C is provided. The opening and closing amount of the damper is controlled so that the air volume becomes uniform. However, the air volume controller 3
Is not necessary, but is preferably provided to stably supply a large amount of air and increase water intake efficiency. The number branched by the air volume controller 3, the size of the branch pipe, and the like can be appropriately selected.
【００１２】フィルター４によって除塵された大気は、
吸引ポンプ２から取り入れられた大量の大気から効率よ
く湿分を取出すために大気圧力を低減するための大気圧
力低減機構たる多孔質通気体５に送給される。前記大気
湿度変換機１は、この多孔質通気体５と、冷却機構６か
らの冷却部７と、冷却され凝縮された水を殺菌する殺菌
装置８と、殺菌された水を採取するための取水口９と、
取り入れた空気を排出する空気排出口１０とから構成さ
れている。前記多孔質通気体５は、種々の形態のものを
採用できるが、大気が加温されて温風になっているの
で、発泡ポリウレタン製、発泡ポリプロピレン製などの
通気体（５０〜１２０メッシュ）を使用することが好ま
しい。尚、図中９ａは水を取り出すための取水バルブで
ある。又、冷却機構６は、一般に用いられている冷却装
置をそのまま使用することができ、例えば、冷媒を圧縮
する圧縮器１１と、ファン１４を有する凝縮器１２と、
減圧機構（図示せず）と冷熱を蓄熱する蓄熱槽（図示せ
ず）等とからなっていて、冷熱を有する冷媒を、配管１
３を介して大気湿度変換機１の冷却部７に搬送するよう
になっている。これによって、取り入れられた大量の大
気を効果的に凝縮して、水を得ることができるのであ
る。尚、冷媒としては、アンモニア、フレオン、水等種
々のものを使用することができる。得られた水は飲料用
に供するため、更に、殺菌装置８に送られて、殺菌され
取水されることとなる。もっとも、得られた水を飲料用
に供するのでなければ、必ずしも殺菌装置８を設けてお
く必要はない。要は、目的に応じて必要設備を設ければ
よい。The air removed by the filter 4 is
In order to efficiently extract moisture from a large amount of air taken in from the suction pump 2, the moisture is supplied to a porous ventilation body 5 which is an atmospheric pressure reducing mechanism for reducing atmospheric pressure. The atmospheric humidity converter 1 includes the porous ventilation body 5, a cooling unit 7 from a cooling mechanism 6, a sterilizer 8 for sterilizing water that has been cooled and condensed, and a water intake for collecting sterilized water. Mouth 9;
And an air discharge port 10 for discharging the taken-in air. The porous ventilation body 5 can adopt various forms. However, since the air is heated to generate warm air, a ventilation body (50 to 120 mesh) made of foamed polyurethane or foamed polypropylene is used. It is preferred to use. In the figure, reference numeral 9a denotes a water intake valve for taking out water. The cooling mechanism 6 can use a generally used cooling device as it is, for example, a compressor 11 for compressing a refrigerant, a condenser 12 having a fan 14,
A refrigerant having a low temperature is supplied to the pipe 1 by a pressure reducing mechanism (not shown) and a heat storage tank (not shown) for storing cold heat.
3, and is conveyed to the cooling unit 7 of the atmospheric humidity converter 1. As a result, water can be obtained by effectively condensing a large amount of air taken in. Various refrigerants such as ammonia, freon, and water can be used as the refrigerant. The obtained water is further sent to a sterilizing device 8 to be sterilized and taken for use in drinking. However, unless the obtained water is used for drinking, it is not always necessary to provide the sterilizer 8. In short, what is necessary is just to provide necessary equipment according to the purpose.
【００１３】[0013]
【実施例】次に、上記実施形態に示す装置によって得ら
れた実施例を、以下に示す。室温５℃で相対湿度７０％
の大気中において、大気吸引ポンプ（吸引能：１分当た
り２４ｍ3 ）で吸引した大気を加温装置によって約４０
℃に昇温させ、この温度に維持しつつ吸引ポンプを長時
間運転した。このときの圧縮した大気圧力は９ｋｇｆ／
ｃｍ2 であった。その結果、平均１０リットル／時の真
水が得られた。この値はほぼ満足できるものであり、大
気が低温である冬季あるいは寒冷地で使用する場合で
も、実用に供することができる結果が得られた。Next, examples obtained by the apparatus shown in the above embodiment will be described below. 70% relative humidity at 5 ° C room temperature
In the atmosphere, the air suctioned by an air suction pump (suction capacity: 24 m 3 per minute) was applied to a heating device for about 40
C., and the suction pump was operated for a long time while maintaining this temperature. The compressed atmospheric pressure at this time is 9 kgf /
cm 2 . As a result, an average of 10 liters / hour of fresh water was obtained. This value was almost satisfactory, and a result was obtained which could be put to practical use even in the case where the air temperature was low in winter or in cold regions.
【００１４】〔別実施の形態〕 （１） 上記実施形態では、制御装置Ｃが加温装置２ａ
の温度制御および風量調節機３内のダンパーの開閉を制
御するようになっているが、いずれか一方のみを制御す
るものでもよく、更に、フィルター４に送給される各分
岐管毎の大気温度を測定し、その結果に基づいて加温装
置２ａの温度制御を行う方式のものでもよい。このよう
になっていると、大気圧力低減機構５へ送る大気から一
層効率のよい取水ができて好ましい。[Another Embodiment] (1) In the above embodiment, the control device C is the heating device 2a
The temperature control and the opening / closing of the damper in the air volume controller 3 are controlled. However, it is also possible to control only one of the temperature control and the air temperature of each branch pipe fed to the filter 4. May be measured, and the temperature of the heating device 2a may be controlled based on the measurement result. This is preferable because water can be more efficiently taken from the atmosphere sent to the atmospheric pressure reducing mechanism 5.
【００１５】（２） 大気圧力を低減するための多孔質
通気体４としては、ある程度の連続加温状態に耐えられ
るものであれば、各種エアフィルター等を用いることも
できる。多孔質通気体の代わりに、大気取り入れ通路に
邪魔板を多数配置するように構成してもよく、オリフィ
スのような構成としてもよい。要は、取り入れる大気圧
力を低減するために、圧損を大きくできる構成であれば
よい。前記多孔質通気体が多孔質焼結材のようなもので
もよい。大気圧力低減機構が、取り入れた大気をらせん
管のような細長い通路を通過させた後、体積の大きな室
に導入することにより大気圧力を低減させるようにした
ものであってもよい。(2) As the porous ventilation body 4 for reducing the atmospheric pressure, various air filters and the like can be used as long as they can withstand a certain continuous heating state. Instead of the porous ventilation body, a large number of baffle plates may be arranged in the air intake passage, or a configuration like an orifice may be used. In short, any structure that can increase the pressure loss in order to reduce the atmospheric pressure to be taken may be used. The porous ventilation body may be a material such as a porous sintered material. The atmospheric pressure reducing mechanism may reduce the atmospheric pressure by passing the taken-in atmosphere through an elongated passage such as a spiral tube, and then introducing the introduced atmosphere into a chamber having a large volume.
【００１６】（３） 取り入れられた大量の大気を効果
的に凝縮させるため、露結を容易にさせる触媒作用を備
えた凝縮剤のようなものを添加してもよい。更に、大気
を冷却して取水した後は外部に逃がす大気中の湿分をで
きるだけ少なくするために、出口部分の大気圧力を高め
るように出口の大きさを小さく絞るようにしてもよい。(3) In order to effectively condense the large amount of air taken in, a condensing agent having a catalytic action to facilitate dew condensation may be added. Furthermore, in order to minimize the moisture in the atmosphere that escapes to the outside after cooling and taking in water, the size of the outlet may be reduced so as to increase the atmospheric pressure at the outlet.
【００１７】（４） 本発明により得られた水は、飲料
用水のみならず各種冷却水、洗浄水等の工業用水として
使用することもできる。(4) The water obtained by the present invention can be used not only as drinking water but also as industrial water such as various kinds of cooling water and washing water.
【図１】本発明に係る取水装置の概略全体構成図FIG. 1 is a schematic overall configuration diagram of a water intake device according to the present invention.
１ 大気湿度変換機 ２ 大気取入装置 ２ａ 加温装置 ３ 風量調節装置 ５ 大気圧力低減機構 ７ 冷却部 ９ 取水口 Ｃ 制御装置 DESCRIPTION OF SYMBOLS 1 Atmospheric humidity converter 2 Atmospheric intake device 2a Heating device 3 Air volume control device 5 Atmospheric pressure reduction mechanism 7 Cooling unit 9 Intake port C control device
Claims (4)
可能な加温装置と、前記大気取入装置によって取り入れ
られる大気圧力を低減する機構を備えると共に取り入れ
られた大気を冷却して湿分を取出す冷却部を内蔵した大
気湿度変換機と、この大気湿度変換機によって得られる
水を取出す取水口とを有する取水装置。An air intake device, a heating device capable of raising the temperature of an intake air, a mechanism for reducing an atmospheric pressure introduced by the air intake device, and a cooling device for cooling the introduced air to obtain a wet air. An intake device having an atmospheric humidity converter having a built-in cooling unit for extracting water, and an intake for extracting water obtained by the atmospheric humidity converter.
気を流量調節するための風量調節装置を備える請求項１
の取水装置。2. An air flow adjusting device for adjusting a flow rate of air taken in by the air intake device.
Water intake equipment.
装置の加温条件とを制御可能な制御装置を備える請求項
２の取水装置。3. The water intake device according to claim 2, further comprising: a control device capable of controlling a post-blow volume of the air volume control device and heating conditions of the heating device.
設けられた５０〜１２０メッシュの多孔質通気体である
請求項１〜３のいずれかの取水装置。4. The water intake device according to claim 1, wherein the atmospheric pressure reducing mechanism is a 50-120 mesh porous ventilation body provided at an air intake.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28540298A JP4593698B2 (en) | 1998-10-07 | 1998-10-07 | Water intake equipment |
| TW88100265A TW384336B (en) | 1998-10-07 | 1999-01-08 | Water capturing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28540298A JP4593698B2 (en) | 1998-10-07 | 1998-10-07 | Water intake equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000110201A true JP2000110201A (en) | 2000-04-18 |
| JP4593698B2 JP4593698B2 (en) | 2010-12-08 |
Family
ID=17691070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28540298A Expired - Fee Related JP4593698B2 (en) | 1998-10-07 | 1998-10-07 | Water intake equipment |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP4593698B2 (en) |
| TW (1) | TW384336B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009537714A (en) * | 2006-05-15 | 2009-10-29 | アイランド スカイ コーポレーション | Multipurpose adiabatic potable water production apparatus and method |
| JP2011151032A (en) * | 2011-03-22 | 2011-08-04 | Eneos Celltech Co Ltd | Fuel cell system |
| JP2014223589A (en) * | 2013-05-16 | 2014-12-04 | 株式会社廣林 | Filter device and water purifier |
| US20160089616A1 (en) * | 2013-05-16 | 2016-03-31 | All Round Corporation | Moisture- harvesting device |
| CN107975961A (en) * | 2017-12-26 | 2018-05-01 | 中国海洋大学 | Utilize the air conditioner refrigerating of fume afterheat and solar energy and the sea water desalination circulatory system |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6247021B2 (en) * | 2013-05-16 | 2017-12-13 | 株式会社Ｍｉｚｕｈａ | Water intake equipment |
| TWI764748B (en) * | 2021-06-04 | 2022-05-11 | 虞碩蛟 | Balloon rain device |
-
1998
- 1998-10-07 JP JP28540298A patent/JP4593698B2/en not_active Expired - Fee Related
-
1999
- 1999-01-08 TW TW88100265A patent/TW384336B/en not_active IP Right Cessation
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009537714A (en) * | 2006-05-15 | 2009-10-29 | アイランド スカイ コーポレーション | Multipurpose adiabatic potable water production apparatus and method |
| JP2011151032A (en) * | 2011-03-22 | 2011-08-04 | Eneos Celltech Co Ltd | Fuel cell system |
| JP2014223589A (en) * | 2013-05-16 | 2014-12-04 | 株式会社廣林 | Filter device and water purifier |
| US20160089616A1 (en) * | 2013-05-16 | 2016-03-31 | All Round Corporation | Moisture- harvesting device |
| CN107975961A (en) * | 2017-12-26 | 2018-05-01 | 中国海洋大学 | Utilize the air conditioner refrigerating of fume afterheat and solar energy and the sea water desalination circulatory system |
| CN107975961B (en) * | 2017-12-26 | 2023-09-26 | 中国海洋大学 | Air conditioner refrigeration and sea water desalination circulating system utilizing flue gas waste heat and solar energy |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4593698B2 (en) | 2010-12-08 |
| TW384336B (en) | 2000-03-11 |
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